微生物膜好氧厌氧联合处理提高造纸厂出水水质的反应器研究

IF 5.4 Q2 ENGINEERING, ENVIRONMENTAL
Nilam Vaghamshi , M.N. Reddy , Kamlesh Shah , Srinivas Murty Duggirala , Pravin Dudhagara
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引用次数: 0

摘要

纸浆和造纸厂由于在造纸过程中产生大量有害废水而严重造成水污染。出水高度浓缩,含有高水平的化学需氧量(COD)、生化需氧量(BOD)、氯化化合物、颜色、悬浮物、木质素及其衍生物。针对造纸废水的处理问题,研究了生物处理对造纸废水中污染物的降解效果。我们筛选了7种真菌和4种放线菌的水解酶,并使用宏基因组学研究对源自牛瘤胃液的厌氧生物膜进行了分类和功能表征。基于一级单段处理对COD的去除效果,在间歇工艺中进行了二级和三级处理。间歇式反应器的第一步是采用厌氧反应器分解填料床厌氧反应器(PBAR)中的主要污染物,从而大大降低了COD。随后在顺序床反应器(SBR)中进行放线菌生物膜的好氧处理,最后在移动床生物膜反应器(MBBR)中进行间歇处理真菌生物膜。通过测量COD的减少来评估每个阶段的有效性。单阶段真菌、放线菌和厌氧生物膜处理在168小时内分别从初始浓度11500 mg/L去除了94.09%、95.30%和95.91%的COD。动力学分析表明,Grau二阶模型准确地描述了所有三个反应器处理的COD去除率。两阶段真菌-放线菌处理和真菌-厌氧处理在初始浓度23,500 mg/L的基础上,在72 h内将COD分别降低了99.82%和98.76%,并改善了其他相关参数。采用厌氧-放线菌-真菌一体化处理工艺,在168 h内有效去除高浓度出水中COD 98.86%、BOD 99.23%、木质素92.16%、色度94.02%。处理后出水达到监管部门规定的标准,可无风险排放到环境中。研究表明,该方法可为工业提供低强度至高强度废水的可持续解决方案。根据废水的COD水平,该研究为工业提供了实施单阶段、两阶段或三阶段处理的选择。事实证明,这种综合方法对纸浆和造纸厂的废水处理具有成本效益和环保的解决方案,显示出大规模工业应用的潜力。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Aerobic and anaerobic integrated treatment using microbial biofilm to improve the quality of the paper mills effluent: A reactor-based study

Aerobic and anaerobic integrated treatment using microbial biofilm to improve the quality of the paper mills effluent: A reactor-based study
The pulp and paper mills significantly contribute to water pollution due to the large quantities of hazardous effluent generated during paper production. The effluent is highly concentrated and contains high levels of chemical oxygen demand (COD), biochemical oxygen demand (BOD), chlorinated compounds, color, suspended materials, lignin, and their derivatives. To address the issue of effluent treatment, the present study investigated the effectiveness of biological treatment to degrade the pollutants of paper mill effluent. We screened seven fungi and four actinomycetes for hydrolase enzymes and used a metagenomics study to taxonomically and functionally characterize the anaerobic biofilm originating from cattle rumen fluid. Based on the COD removal efficiency of the primary single-stage treatment, we implemented two- and three-stage treatments in batch process. The first step in an integrated approach using batch reactors was an anaerobic reactor to break down primary pollutants in a packed bed anaerobic reactor (PBAR), which greatly reduced COD. This was followed by aerobic treatment with actinomycetes biofilm in a sequential bed reactor (SBR), and finally, fungal biofilm treatment in a moving bed biofilm reactor (MBBR) in batch process. The effectiveness of each stage was assessed by measuring the reduction of COD. Single-stage fungal, actinomycetes, and anaerobic biofilm treatment removed 94.09 %, 95.30 %, and 95.91 % COD, respectively, from an 11,500 mg/L initial concentration within 168 h. Kinetic analysis demonstrated that the Grau second-order model accurately described COD removal across all three-reactor treatment. Two-stage fungal-actinomycetes and fungal-anaerobic treatments reduced COD by 99.82 % and 98.76 %, respectively, from a 23,500 mg/L initial concentration within 72 h while also improving other relevant parameters. An integrated anaerobic-actinomycetes-fungal treatment process effectively removed 98.86 % COD, 99.23 % BOD, 92.16 % lignin, and 94.02 % color from a high-strength effluent within 168 h. After the treatment process, the effluent meets the standard given by regulatory agencies and can be discharged into the environment without any risks. The study demonstrated that industries can implement the method to provide sustainable solutions for low- to high-strength effluents. Based on the COD levels of the effluent, the study gives industries the option to implement single, two, or three-stage treatments. The integrated approach proved to be a cost-effective and eco-friendly solution for pulp and paper mill effluent treatment, demonstrating potential for large-scale industrial applications.
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Journal of hazardous materials advances
Journal of hazardous materials advances Environmental Engineering
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